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CARBON DIOXIDE DRIVEN PH REFERENCE METHOD FOR TRANSFER AND SCALING OF FERMENTATION PROCESSES

机译:发酵过程的转移和缩放二氧化碳驱动pH参考方法

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For the last decades, engineering aspects were in the focus for scale up, scale down as well as transfers of fermentation processes. For cell culture processes however, comparability of process parameters like pCO_2, lactate concentration, growth rates, base addition and ultimately product concentration and quality attributes between large and small scale was not sufficiently addressed by those parameters alone. On the other hand, parameters exist like pH and dissolved oxygen, that are both equipment and location independent and that are usually maintained by respective control loops. Especially pH has been proven to be of particular significance for process performance, and therefore for scaling purposes as well. The current standard approach to monitor and adjust bioreactor probes however relies on sample based pH offline reading. pH in a sample depends on a variety of parameters like CO_2 degassing, temperature, overall respiration of suspended cells and the like, and might differ from the actual bioreactor pH after sampling. Adding to that, offline measurement methods might deliver different results depending on device type, probe age, media properties, daily adjustment procedures, response times, operator effects and so on. Clearly, the sum of those offsets cannot be detected or quantified using the very same sample based pH offline measurement that introduces those offsets in the first place. Direct cross-site comparison of pH values that are desperately needed for efficient process transfer is impossible in required accuracy, relying on sample based pH offline measurement. To decrease the risk of process variability and potential quality issues, increase efficiency of troubleshooting, scaling and process transfers a method that allows detecting otherwise undetectable pH offsets is essential. In this work, we present a carbon dioxide based alternative method that allows challenging the standard approach, and is able to establish comparable pH values globally by decreasing dependency onto sample based pH offline measurement. In cell free culture media, a bioreactor state where carbon dioxide addition equals carbon dioxide removal leads to stable pH and a net carbon dioxide mass transfer between the gas phase and the liquid phase of zero. In this case, carbon dioxide concentration in the gas phase is not any more a function of parameters that influence mass transfer kinetics, and can therefore be considered scale independent. We have shown that pH values that are derived from this chemical relation are superior to standard sample based pH offline reading, and are able to decrease process variability and increase comparability of process performance between runs, scales and sites. Furthermore, troubleshooting efforts as well as process development are a lot more effective, if pH as one key parameter that adds to process variability can be knocked out or at least quantified. Major automation opportunities in scale down model development like fully automated carbon dioxide removal control strategies that massively depend on comparable pH controller behavior were developed. Phase Ⅲ development of a late stage project delivering bispecific antibodies already was performed exclusively relying on this carbon dioxide based pH reference method. Another project did switch to this method during phase Ⅲ development to enable more efficient process development. Scale up has been performed successfully up to 400L scale, feasibility studies were performed in 12K scale in three different projects. Results out of this data will be presented, including important considerations for this kind of approach.
机译:在过去的几十年中,工程方面处于缩小,缩小,缩小和发酵过程的转移。然而,对于细胞培养方法,单独的参数,PCO_2,乳酸盐浓度,生长速率,碱基加成和最终产品浓度和最终产品浓度和质量属性的可比性并不能通过那些参数充分解决。另一方面,参数存在于pH和溶解的氧气上,其是设备和位置无关,并且通常由各自的控制回路保持。特别是pH已被证明对流程性能特别重要,因此也用于缩放目的。然而,监测和调整生物反应器探针的目前的标准方法依赖于基于样品的pH离线读数。样品中的pH取决于多种参数,如CO_2脱气,温度,悬浮电池的总体呼吸等,并且可能与取样后的实际生物反应器pH不同。此后,离线测量方法可以根据设备类型,探测年龄,媒体属性,日常调整程序,响应时间,操作员效果等提供不同的结果。显然,使用基于样品的pH离线测量的离线测量,不能检测或量化这些偏移的总和,该测量首先引入这些偏移。在所需的精度下,依赖于基于样品的pH离线测量,不可能对有效的过程传递绝望地进行pH值的直接横向位点比较。为了降低过程变异性和潜在质量问题的风险,提高故障排除效率,缩放和过程转移一种方法,该方法允许检测到否则无法检测的pH偏移是必不可少的。在这项工作中,我们介绍了一种基于碳二氧化碳的替代方法,其允许挑战标准方法,并且能够通过将基于样品的pH离线测量降低到样本的pH离线测量来全局建立类似的pH值。在细胞自由培养基中,二氧化碳添加等于二氧化碳除去的生物反应器状态,以稳定的pH和气相与零液相之间的净二氧化碳质量传递。在这种情况下,气相中的二氧化碳浓度不再有任何影响传质动力学的参数的功能,因此可以被认为是独立的规模。我们已经表明,从这种化学关系导出的pH值优于标准的基于样品的pH离线读数,并且能够降低过程变异性并增加运行,尺度和站点之间的过程性能的可比性。此外,如果pH作为增加处理可变性的一个关键参数,可以敲除或至少量化,则努力以及过程开发的故障排除以及过程开发的努力更有效。大规模自动化机会规模落下的模型开发,如全自动二氧化碳去除控制策略,依赖于可比的pH控制器行为。已经依赖于这种基于二氧化碳的pH参考方法,进行了递送双特异性抗体的后期抗体的阶段Ⅲ期开发。在Ⅲ期开发期间,另一个项目确实切换到这种方法,以实现更有效的过程开发。已经成功地进行了扩展,最高可达400L规模,可行性研究在三个不同的项目中以12K规模进行。将出现此类数据的结果,包括这种方法的重要考虑因素。

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